EP0406903B1 - Granulating and coating apparatus and granulating and coating method using the same - Google Patents
Granulating and coating apparatus and granulating and coating method using the same Download PDFInfo
- Publication number
- EP0406903B1 EP0406903B1 EP90112971A EP90112971A EP0406903B1 EP 0406903 B1 EP0406903 B1 EP 0406903B1 EP 90112971 A EP90112971 A EP 90112971A EP 90112971 A EP90112971 A EP 90112971A EP 0406903 B1 EP0406903 B1 EP 0406903B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coating
- article
- granulating
- coating material
- coated
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/94—Liquid charges
- B29B7/945—Liquid charges involving coating particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/003—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic followed by coating of the granules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
- B01J2/04—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Glanulating (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
Description
- This invention relates to granulating and coating techniques and more particularly to techniques effective for use in granulating, coating, drying, etc. of a powdery or granular material having a relatively minute particle diameter.
- In general, as the granulation coating techniques of the type described, such an arrangement is thought of that a raw powdery or granular material as being an article to be coated and coating liquid as being a coating material are supplied from positions opposed to each other in a diameter direction of the apparatus, and drying air streams such as hot air are supplied from underside thereof.
- Now, in the aforesaid techniques, the article to be coated and the coating material collide against each other from the directions opposed to each other. Moreover, in this type of collision against each other from the opposed directions, due to the imbalance in flow-out forces of the article to be coated and of the coating material, one of the article and the coating material tends to become stronger in the force of collision than the other.
- For this reason, for example, when the blow-out force of the coating material is stronger than that of the article, such disadvantages tend to occur that the coating material adheres to the opposed inner wall surface of the apparatus and is solidified thereon, or the article adheres to the coating material before the coating material is solidified, and is accumulated thereon.
- Furthermore, there is a fear that such a disadvantage may occur that, due to the imbalance in the blow-out forces or blow-out flow rates, the coating liquid itself is turned into solid particles due to a so-called "spray-dry" phenomenon, without adhereing onto the article to be coated.
- It is an object of the present invention to provide techniques capable of performing reliable granulation coating.
- It is another object of the present invention to provide techniques capable of preventing adhering and solidification of the coating material on the opposed inner wall surface, or turning the coating material into particles due to the so-called "spray-dry" phenomenon.
- The above-described and other objects and the novel characteristics of the present invention will be made further apparent from the following description and the accompanying drawings.
- The outline of the typical apparatus according to the present invention is briefly described as follows.
- Namely, the granulating and coating apparatus and granulating and coating method using the same according to the present invention are arranged such the drying air streams are supplied on the way from collision of the article to be coated and the coating material to catching of the coated article.
- Furthermore, respective means of supplying the article to be coated and the coating material can be parallelly provided at adjacent positions where air streams dispersed form the both supply means are not in contact with the other means respectively.
- With the granulating and coating apparatus and granulating and coating method using the same according to the present invention, the article to be coated and the coating material are not flown out to the opposed inner wall surfaces from the opposed directions, so that adhering and solidificaton of the article to be coated and/or the coating material to the opposed inner wall surfaces due to the imbalance in the opposed blow-out forces, or accumulation of the coating material, which is turned into solid particles due to the "spray dry" phenomenon are prevented from occurring, thus enabling to perform reliable granulation and coating.
- Fig. 1 is a schematic explanatory view showing an embodiment of the granulating and coating apparatus according to the present invention;
- Fig. 2 is an explanatory view showing an example of the method of feeding drying air streams;
- Fig. 3 is a schematic view showing the essential portions of the granulating and coating apparatus according to another embodiment of the invention; and
- Fig. 4 is a schematic sectional view showing the essential portions of a further embodiment of the granulating and coating apparatus according to the invention.
- Referring to Figs. 1 and 2, with a granulating and coating apparatus according to the invention, a
processing cylinder 1 as being a main body of the apparatus for performing therein granulating, coating, drying, etc. of a powdery or granular material has a cylindrical shape in a horizontal cross-section as shown in Fig. 2 for example. - On a bottom wall of this processing cylinder, a spray nozzle, i.e. a powdery or granular material nozzle 2 (supply means) for feeding the powdery or granular material as being an article to be coated and an spray nozzle, i.e. a liquid nozzle 3 (supply means) for feeding a coating liquid as being a coating material are parallely provided at positions adjacent to each other and directed upward in the
processing cylinder 1. Namely, thesenozzles respective nozzles air sources - On the other hand, air-stream flow-in
openings 6 for feeding drying air streams are opened at a side surface portion in the substantially intermediate area of theprocessing cylinder 1. The drying air streams are generally a hot air or cooled air. In each channel to the respective air-stream flow-inopenings 6, there is independently provided flow-rate control means such for example as damper which controls air flow rate to the respective air-stream flow-inopenings 6 independently of one another. - In this embodiment, the air-stream flow-in
openings 6 are provided at positions upwardly of the powdery orgranular material nozzle 2 and theliquid nozzle 3, i.e. at the downstream side thereto, whereby the drying air streams are fed into theprocessing cylinder 1 after the article to be coated and the coating material have collided on each other in the directions of parallel flowing. - Furthermore, as shown in Fig. 2, the air streams from the air-stream flow-in
openings 6 are supplied from directions tangent to theprocessing cylinder 1 of cylindrical shape, so thatvolute air streams 6a are formed in the processing cylinder. Because of these volute air streams, a contact time between the coated articles and the drying air is elongated, and adhesion of the powdery or granular material and the coating liquid to the inner wall surfaces of theprocessing cylinder 1 can be prevented. - Further, in the upper portion of the
processing cylinder 1, there is opened acatching channel 8, and coatedproducts 9, on which the treating such as granulating, coating, drying, etc. has been completed in theprocessing cylinder 1, are attracted from the interior of theprocessing cylinder 1 to the outside thereof through thecatching channel 8 by an attracting force of ablower 10 or the like. - The
products 9 attracted to the outside of theprocessing cylinder 1 through thecatching channel 8, then, descend in acyclone 11, pass through arotary valve 12 and are caught by areceiving vessel 13. While, minute particles, dust, etc. not usable as the products do not descend in thecyclone 11 and are caught and removed by abag filter 14. - Action of this embodiment will hereunder be described.
- The powdery or granular material as being the article to be subjected to granulating and coating treatment and the coating liquid as being the coating material are blown out into the
processing cylinder 1 through the powdery orgranular material nozzle 2 and theliquid nozzle 3, respectively. At this time, the blow-out forces through therespective nozzles air sources - The article to be coated and the coating liquid are blown out in directions to the top wall of the
processing cylinder 1 in flows parallel to each other and collide on each other, so that the coating liquid is uniformly coated around the articles, and granulating and coating are performed. - In that case, the coating liquid and the article to be coated are not blown out in the directions opposed to each other and not blown out to the inner wall surfaces of the
processing cylinder 1, so that the blown-out force of either one of the coating liquid and the article does not become by far larger or by far smaller than the other, namely, adhesion of the coating liquid and the article to the inner wall surfaces of theprocessing cylinder 1 due to the imbalance of the blown-out forces can be suppressed. Furthermore, the "spray-dry" phenomenon, where the coating liquid is accumulated itself and turned into the solid particles, can be suppressed. - On the other hand, in the
processing cylinder 1, the drying air streams are fed through the air-stream flow-inopenings 6 into a drying zone positioned upwardly of a coating zone formed by thenozzles openings 6 are controlled by the flow-rate control means 7 independently of each other. - By the supply of the drying air streams, the articles which have been coated with the coating material are dried to a desired dryness.
- At that time, the drying air streams are supplied through the air-stream flow-in
openings 6 from the direction tangent to theprocessing cylinder 1 as shown in Fig. 2, so that the contact time between the coated products and the drying air streams is elongated, and adhesion of the coating liquid and the articles to be coated to the inner wall surface of theprocessing cylinder 1 can be effectively suppressed by the forming of the substantiallyvolute air streams 6a. - As described above, the coating zone is formed by the blow-outs of the articles to be coated and the coating liquid through the
nozzles openings 6. These two zones are separated, so that the spray-dry phenomenon, in which the coating liquid itself is accumulated and turned into the particles, can be prevented from occurring. - As described above, the coated
products 9, on which granulating, coating and drying have been completed, are passed through the catchingchannel 8 from theprocessing cylinder 1 and attracted to thecyclone 11 under the attracting force of theblower 10. - In the
cyclone 11, thenon-defective products 9 having the given quality and the given quantity descend in thecyclone 11, are passed through therotary valve 12 and received in thereceiving vessel 13. - On the other hand, the minute particles, dust, etc. attracted into the
cyclone 11 are further attracted into thebag filter 14 through the top portion of thecyclone 11 under the attracting force of theblower 10, caught by thebag filter 14 and removed to the outside of a system. - Fig. 3 is the schematic view showing the essential portions of a second embodiment of the granulating and coating apparatus according to the present invention.
- In this second embodiment, the article to be fed to the powdery or
granular material nozzle 3 is stored inhopper 15, delivered under pressure to the powdery orgranular material nozzle 2 by the blow-out force of the compressed air from thecompressed air source 4, and blown out into theprocessing cylinder 1 through thenozzle 2. - Furthermore, in this second embodiment, both of the powdrey or
granular material nozzle 2 and theliquid nozzle 3 are parallelly provided at adjacent positions and directed upwardly toward the top wall, in the bottom portion of theprocessing cylinder 1, not on the bottom wall itself of theprocessing cylinder 1. It goes without saying that, also in this second embodiment, thenozzles - Further, in this second embodiment, the air-stream flow-in
openings 6 are disposed to feed the drying air streams into theprocessing cylinder 1 in the the opposed directions to each other, not in the same directions. - In this second embodiment also, the coating zone formed by the
nozzles openings 6 for the dry air streams are provided on the way from the completion of coating to the catching, so that such disadvantages can be reliably controlled as adhesion of the coating material and the article to be coated to the inner wall surfaces of theprocessing cylinder 1 and turning the coating material into the particles due to the spray-dry phenomenon. - Fig. 4 is the schematic sectional view showing the essential portion of a third embodiment of the granulating and coating apparatus according to the present invention.
- In this third embodiment, the powdery or
granular material nozzle 2 and theliquid nozzle 3 are provided at the top wall of theprocessing cylinder 1, not at the bottom wall, and are directed downward. - Furthermore, in accordance with the
nozzles catching channel 8 is provided at the bottom portion of theprocessing cylinder 1, and the air-stream flow-inopenings 6 are opened between thenozzles catching channel 8. - The
nozzles openings 6 and thecatching channel 8 are arranged conversely in the vertical direction between this third embodiment and the first and second embodiments. However, coating, drying, and the like of the article to be coated and the coating material are identical in order with those in the second embodiments. And, such functional effects as prevention of adhesion of the coating material and the like to the inner wall surfaces of theprocessing cylinder 1 and prevention of turning the coating material into the solid particles can be obtained similarly to the first and second embodiments. - The invention achieved by the present inventor has been described in detail with reference to the embodiments, however, the present invention should not be limited to the above embodiments and is variable in many ways within the scope of the claims.
- For example, the positions of installation of the
nozzles catching channel 8 and the directions of the air-stream flow-inopenings 6 may be changed into those other than in the above embodiments. - Furthermore, the number of the air-stream flow-in
openings 6 may be one or a plural number. - Further, the sectional shape of the
processing cylinder 1 should not be limited to that in the above embodiments. - The forgoing description has been given of the case where the invention achieved by the present inventor is applied to granulating, coating and drying of the pharmaceuticals, food products, beauty preparations and chemical products which are included in the field of applicability, however, the application of the invention should not be limited to this, and the invention is applicable to granulating, coating, drying and so on of other materials.
- The following is the brief description of the advantages obtained by the typical invention out of the inventions disclosed in the present application.
- The drying air-stream flow-in openings are provided on the way from the collision of the article and the coating material to the catching, whereby the article to be coated and the coating material are not blown out to the opposed inner wall surfaces from the directions opposed to each other and the parallel flows are formed, so that adhesion of the coating material and the article to be coated to the opposed inner wall surfaces of the processing cylinder due to the imbalance of the opposed blow-out forces and solidification thereon can be suppressed.
- The coating zone and the drying zone are separated, whereby, the "spray dry" phenomenon where the coating material itself is accumulated and turned into the solid particles is prevented. Therefore, the reliable granulating and coating can be performed.
- Respective means for supplying the article to be coated and the coating material use the compressed air independently from each other. And, the respective supply means can be adjusted independently of each other, thus enabling to obtain the optimum blow-out forces.
- The means for supplying the article to be coated and the coating material are parallelly provided at the adjacent positions where the air stream dispersed from respective means is not in contact with the other supplying means, so that the parallel flows are formed in the processing cylinder and adhesion of the coating material and the like to the inner wall surfaces of the processing cylinder can be more reliably suppressed.
- A section of the channel from the collision of the article to be coated and the coating material to the catching thereof is substantially circular, and the flow-in direction of the drying air streams are tangent to the circular section, so that the contact time between the coated article and the drying air streams can be elongated. And moreover, adhesion of the coating material and the like to the inner wall surface can be more effectively suppressed by the formation of the substantially volute air streams.
- When, at least two drying air-stream flow-in openings are provided and each of the openings is provided with a means for independently controlling the air flow rate, the optimum drying can be made by the optimum flow rate at all times by the independent control of the air flow rates from the respective flow-in openings.
Claims (5)
- A granulating and coating apparatus performing granulating, coating and drying by use of drying air streams, which comprises:
a means for supplying an article to be coated,
a means for supplying a coating material, and
one or plurality of drying air-streams flow-in openings, characterized in that
said means for supplying an article to be coated and said means for supplying a coating material are provided at such positions that said article and said coating material collide on each other before the article and the coating material are dispersed by the drying air streams, and
said one or plurality of drying air-streams flow-in openings are provided on the way from the collision of said article and said coating material to the catching thereof; furtheron said means for supplying the article to be coated and said means for supplying coating material are compressed airsources (4, 5) independently from each other;
and said means for supplying said article and said means for supplying coating material are parallely provided at adjacent positions in such a manner that each means is not in contact with a respective air stream dispersed from the other means. - The granulating and coating apparatus as set forth in claim 1, characterized in that:
a section of a channel 1 from the collision of said article and said coating material to the catching thereof is substantially circular, and the flow-in directions of the drying air streams are tangent to the circular section. - The granulating and coating apparatus as set forth in claim 1, characterized in that:
at least two drying air-stream flow-in openings are provided, and each of which is provided with respective means for independently controlling an air flow rate of the respective opening. - A granulating and coating method utilizing a granulating and coating apparatus according to claim 1, characterized in that:
granulating, coating and drying are performed by use of drying air streams,
an article to be coated and a coating material are supplied from respective supply means provided in the granulating and coating apparatus at adjacent positions so that said article and said coating material collide on each other before said article and said coating material are dispersed by the drying air streams, and
the drying air streams are supplied into the granulating and coating apparatus on the way between the collision of articles to be coated and the coating material and the catching thereof. - The granulating and coating method as set forth in claim 4, characterized in that:
a mean particle diameter of said article to be coated is about 250 µm and therebelow.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1176921A JP3031923B2 (en) | 1989-07-07 | 1989-07-07 | Granulation coating apparatus and granulation coating method using the same |
JP176921/89 | 1989-07-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0406903A1 EP0406903A1 (en) | 1991-01-09 |
EP0406903B1 true EP0406903B1 (en) | 1993-09-29 |
Family
ID=16022093
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90112971A Expired - Lifetime EP0406903B1 (en) | 1989-07-07 | 1990-07-06 | Granulating and coating apparatus and granulating and coating method using the same |
Country Status (4)
Country | Link |
---|---|
US (1) | US5096744A (en) |
EP (1) | EP0406903B1 (en) |
JP (1) | JP3031923B2 (en) |
DE (1) | DE69003607T2 (en) |
Cited By (1)
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---|---|---|---|---|
CN109395524A (en) * | 2018-12-19 | 2019-03-01 | 武汉天空蓝环保科技有限公司 | The ultra-clean processing system of flue gas based on particulate matter chemical agglomeration and bag-type dust |
Families Citing this family (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0763606B2 (en) * | 1991-10-18 | 1995-07-12 | フロイント産業株式会社 | Coating equipment |
DK201791D0 (en) * | 1991-12-17 | 1991-12-17 | Boerge Holm Christensen | METHOD OF COATING |
US5662922A (en) * | 1992-01-20 | 1997-09-02 | Christensen; Borge Holm | Iron-containing composition for the prevention of anaemia and a method for producing the composition |
JP2584928B2 (en) * | 1992-02-12 | 1997-02-26 | フクビ化学工業株式会社 | Powder surface reformer |
DE4243438C2 (en) * | 1992-12-22 | 1996-06-05 | Hosokawa Alpine Ag | Method and device for fluid bed jet grinding |
US5598979A (en) * | 1995-04-20 | 1997-02-04 | Vortec, Inc. | Closed loop gradient force comminuting and dehydrating system |
DE19611112C2 (en) * | 1996-03-21 | 2002-04-18 | Jackering Altenburger Masch | Method and device for producing extremely fine powders |
BE1010771A3 (en) * | 1996-11-26 | 1999-01-05 | Lhoist Rech & Dev Sa | Soil treatment compositions, method of preparation and use. |
JPH10192670A (en) * | 1996-12-27 | 1998-07-28 | Inoue Seisakusho:Kk | Dispersion and dispersing apparatus utilizing supercritical state |
AU750866B2 (en) * | 1998-05-22 | 2002-08-01 | Cnh Industrial Canada, Ltd. | In-line seed treating unit for air seeders |
US6394371B1 (en) | 1998-06-19 | 2002-05-28 | Superior Technologies Llc | Closed-loop cyclonic mill, and method and apparatus for fiberizing material utilizing same |
US6517015B2 (en) | 2000-03-21 | 2003-02-11 | Frank F. Rowley, Jr. | Two-stage comminuting and dehydrating system and method |
US6715705B2 (en) | 2001-03-16 | 2004-04-06 | Frank F. Rowley, Jr. | Two-stage comminuting and dehydrating system and method |
NL1020469C2 (en) * | 2002-04-25 | 2003-10-28 | Carlisle Process Systems B V | Spray drying device and feed means for such a spray drying device. |
US6790349B1 (en) | 2003-05-05 | 2004-09-14 | Global Resource Recovery Organization, Inc. | Mobile apparatus for treatment of wet material |
US7674032B2 (en) * | 2004-10-19 | 2010-03-09 | Eastman Kodak Company | Fluidics coating apparatus and method for surface treating of toner and dry inks |
US20080061004A1 (en) * | 2004-10-29 | 2008-03-13 | Loran Balvanz | Method and apparatus for producing dried distillers grain |
US20070007198A1 (en) * | 2005-07-07 | 2007-01-11 | Loran Balvanz | Method and apparatus for producing dried distiller's grain |
AU2007315862A1 (en) * | 2006-06-21 | 2008-05-08 | Martinswerk Gmbh | Coated aluminum hydroxide particles produced by mill-drying |
US7753298B2 (en) * | 2007-01-31 | 2010-07-13 | Vector Corporation | Rotor processor |
US7736409B2 (en) * | 2007-04-27 | 2010-06-15 | Furrow Technologies, Inc. | Cyclone processing system with vortex initiator |
JP5872140B2 (en) * | 2010-03-25 | 2016-03-01 | 住友ベークライト株式会社 | Particle manufacturing method and semiconductor sealing resin composition manufacturing method |
WO2012018638A2 (en) | 2010-07-26 | 2012-02-09 | Biomatrica, Inc. | Compositions for stabilizing dna, rna and proteins in blood and other biological samples during shipping and storage at ambient temperatures |
US9845489B2 (en) | 2010-07-26 | 2017-12-19 | Biomatrica, Inc. | Compositions for stabilizing DNA, RNA and proteins in saliva and other biological samples during shipping and storage at ambient temperatures |
WO2014100755A2 (en) | 2012-12-20 | 2014-06-26 | Biomatrica, Inc. | Formulations and methods for stabilizing pcr reagents |
ES2786373T3 (en) | 2014-06-10 | 2020-10-09 | Biomatrica Inc | Platelet stabilization at room temperatures |
ES2946184T3 (en) | 2015-12-08 | 2023-07-13 | Biomatrica Inc | Reduced erythrocyte sedimentation rate |
CN106179114B (en) * | 2016-08-04 | 2018-09-25 | 浙江华康药业股份有限公司 | A kind of continuous boiling granulator of vertical type full automatic and sugar alcohol prilling process |
CN106732171B (en) * | 2016-11-29 | 2019-01-22 | 浙江兰博生物科技股份有限公司 | A kind of multistage granulation by spraying melted nicotinamide tower and its operation method |
CN106512850B (en) * | 2016-11-29 | 2019-03-08 | 浙江兰博生物科技股份有限公司 | A kind of granulation by spraying melted nicotinamide tower and its operation method |
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FR1333958A (en) * | 1962-07-03 | 1963-08-02 | Nat Dairy Prod Corp | Method and apparatus for the production of powder agglomerates |
GB1052156A (en) * | 1964-05-04 | |||
US3632257A (en) * | 1969-09-04 | 1972-01-04 | Naoyoshi Ashizawa | Apparatus for making granules |
NL7211598A (en) * | 1972-08-25 | 1974-02-27 | Spray dried powder coating plant - with inlet for powder and hot air mixture and sprayer for emulsifier coating | |
US4592302A (en) * | 1984-11-07 | 1986-06-03 | Freund Industrial Co., Ltd. | Coating method and apparatus |
CH664297A5 (en) * | 1985-03-01 | 1988-02-29 | Freunt Ind Co Ltd | APPARATUS FOR GRANULATION AND COATING IN THE FLUIDIZED STATE. |
DE3519309C1 (en) * | 1985-05-30 | 1986-12-18 | Alpine Ag, 8900 Augsburg | Process for the continuous production of granules from a solid in a fluidized material bed |
JPS6274443A (en) * | 1985-09-27 | 1987-04-06 | Toyo Eng Corp | Method for processing particle |
CH666828A5 (en) * | 1985-12-30 | 1988-08-31 | Aeromatic Ag | Device for producing and / or editing granules. |
DE3716968A1 (en) * | 1987-05-20 | 1988-12-01 | Nied Roland | Apparatus for the continuous production of granules |
-
1989
- 1989-07-07 JP JP1176921A patent/JP3031923B2/en not_active Expired - Fee Related
-
1990
- 1990-07-03 US US07/547,933 patent/US5096744A/en not_active Expired - Lifetime
- 1990-07-06 DE DE90112971T patent/DE69003607T2/en not_active Expired - Fee Related
- 1990-07-06 EP EP90112971A patent/EP0406903B1/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109395524A (en) * | 2018-12-19 | 2019-03-01 | 武汉天空蓝环保科技有限公司 | The ultra-clean processing system of flue gas based on particulate matter chemical agglomeration and bag-type dust |
Also Published As
Publication number | Publication date |
---|---|
EP0406903A1 (en) | 1991-01-09 |
JP3031923B2 (en) | 2000-04-10 |
DE69003607T2 (en) | 1994-01-27 |
DE69003607D1 (en) | 1993-11-04 |
JPH0342029A (en) | 1991-02-22 |
US5096744A (en) | 1992-03-17 |
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